In this groups prior work, Bauskar et al. incorporated and removed pore-former (lithium carbonate, LiCO3) to form ~10 μm pores within the anode catalyst layer. [1] Performance was optimized for anode catalyst layer with pores formed from 17.5 wt% LiCO3. However, the size of the pore-former increased catalyst agglomerate separation and reduced the connected electrochemical surface area resulting in reduced formic acid electrooxidation charge transfer activity.
Previous work to incorporate smaller pores via a smaller pore-former (magnesium oxide, MgO, ~50 nm) showed that, at 25 wt% pore-former, the electrochemical surface area and cell performance increased by 293% and 86%, respectfully, compared to an anode catalyst layer with no pore-former. [2] The present study explores a higher range of varying pore-former wt% while also investigating the effects of sonication of the catalyst ink via in-situ catalyst layer characterization, scanning electron microscopy, and catalyst ink rheology.
- Bauskar, A.S. and Rice, C.A., Impact of Anode Catalyst Layer Porosity on the Performance of a Direct Formic Acid Fuel cell. Electrochimica Acta 2012, 62, 36-41.
- Lam, S., Bixby, M.M., and Rice, C.A., Optimization of Mass Transport within Direct Formic Acid Fuel Cell Catalyst Layer via Pore Formers. ECS Trans 2020, 98, 355.